CN212247223U - Electrolytic ozone generator - Google Patents
Electrolytic ozone generator Download PDFInfo
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- CN212247223U CN212247223U CN202020618526.7U CN202020618526U CN212247223U CN 212247223 U CN212247223 U CN 212247223U CN 202020618526 U CN202020618526 U CN 202020618526U CN 212247223 U CN212247223 U CN 212247223U
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 101
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 253
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- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 4
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- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 2
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model discloses an electrolytic ozone generator, which comprises a cavity, an electrode plate and a diaphragm, wherein the electrode plate and the diaphragm are arranged in the cavity; a water inlet and a water outlet are respectively arranged at two ends of the cavity; one side surface of the diaphragm is parallel and opposite to the positive plate, and the other side surface of the diaphragm is parallel and opposite to the negative plate; annular flow guide channels are arranged between the peripheries of the positive plate, the negative plate and the diaphragm and the inner wall of the cavity; a water flow distribution space is arranged between the water inlet and the electrode plate at the water inlet end and is respectively communicated with the annular flow guide channel and the through holes on the electrode plate at the water inlet end; the positive plate and the negative plate are electrically connected through water flowing through the positive plate and the negative plate. The ozone generator can quickly take away prepared ozone, improve the dissolving amount of the ozone in water, further improve the concentration of the ozone, and is stable in operation performance, low in energy consumption and beneficial to heat dissipation of electrode plates.
Description
Technical Field
The utility model relates to an ozone electrolysis unit technical field, concretely relates to electrolysis formula ozone generator.
Background
Ozone (O)3) Is oxygen (O)2) Is a light blue gas with a particular odor. Ozone is a strong oxidant, has strong sterilization and disinfection effects due to strong oxidation capacity, is a widely recognized broad-spectrum efficient sterilization and disinfection agent in the world, and more importantly, generates oxygen after sterilization and disinfection, does not generate secondary pollution, and is a green and environment-friendly disinfectant.
At present, ozone is widely applied in many countries and regions, such as in the industries and fields of drinking water purification, medical water disinfection, air purification, food purification, sewage treatment, planting and breeding industry, paper bleaching and the like, however, ozone is easy to self-decompose and not easy to store, so that ozone is generally prepared and used when being adopted. At present, the main means for producing ozone are corona method, electrolytic method, ultraviolet method, nuclear radiation method, plasma method, and the like. The ozone generation technology which is put into use by enterprises such as food, hospitals and pharmacy mainly comprises a corona discharge method and an electrolysis method. The corona discharge method is a method for generating ozone by discharging dry oxygen-containing gas through corona high voltage, and the technology has high yield of generated ozone and can realize industrial production, but has more defects. In the process of using the corona method for preparation, because gas needs to be dried, a good gas drying and generating device and a cooling system need to be arranged, so that the equipment is huge, the investment cost is high, the movement is inconvenient, the concentration of the produced ozone is low, the volume ratio of the ozone is 1-6%, and the ozone mixture contains a certain amount of carcinogenic substances such as oxynitride and the like; the electrodes are also easily damaged by high-voltage discharge.
At present, in the method for preparing ozone by electrolyzing water at low pressure, an ion exchange membrane and cathode and anode catalyst membranes are mainly adopted to form a membrane electrode assembly, and the membrane electrode assembly is utilized to electrolyze water to generate ozone. For example, patent publication No. CN107177861B discloses an ozone generator nozzle having an anode electrolytic chamber and two cathode electrolytic chambers separated from each other, wherein the anode electrolytic chamber is located at the middle position inside the chamber, and the two cathode electrolytic chambers are located at the left and right sides of the anode electrolytic chamber. Be equipped with positive plate, diaphragm and negative plate between anodal electrolysis chamber and the negative pole electrolysis chamber, wherein the positive plate is in anodal electrolysis intracavity portion, and the negative plate is in negative pole electrolysis intracavity portion, and keeps apart each other through the diaphragm that has insulating properties between anodal electrolysis chamber and the negative pole electrolysis chamber that links to each other. Since the membrane of the shower head is tightly attached to the electrode, it is difficult to flow the ozone water generated by electrolysis, and thus the heat dissipation performance is poor, and the concentration of ozone water generated per unit area cannot be increased.
For example, the invention patent application with the application publication number of CN109487293A discloses an electrolytic structure of an ozone electrolytic chamber, when the electrolytic structure of the ozone electrolytic chamber electrolyzes an electrolytic solution, a water body enters the electrolytic chamber from a water inlet end, then enters a gap between an electrode plate and a membrane of the water inlet end through a through hole of the electrode plate of the water inlet end, then flows to a gap between the membrane and the electrode plate of a water outlet end through the through hole of the membrane or the gap of the membrane, and then flows outwards from the gap between the electrode plates of the water outlet end to the water outlet end or flows towards the direction of the water outlet end through the through hole of the electrode plate of the water outlet end. The above structure has the following disadvantages:
1. this ozone electrolysis room electrolysis structure is at the electrolysis in-process, and rivers are through intaking after the end gets into the electrolysis chamber, and the end electrode piece is directly strikeed into to whole rivers for it is big to intake the end electrode piece range of floating, influences the stability of voltage, makes the electrolysis operation performance unstable.
2. In the process that water flows in the electrolytic chamber, the membrane and the electrode plate at the water outlet end are impacted by the water flow, so that the distance between the electrode plate at the water inlet end and the membrane and the distance between the electrode plate at the water outlet end and the membrane are increased, the working voltage is increased, and the energy consumption is increased.
3. The electrolytic structure of the ozone electrolytic chamber has low water flow speed in the electrolytic process, and is not beneficial to taking away ozone generated by electrolysis and heat dissipation of electrode plates.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the existing problems and provide an electrolytic ozone generator, which has stable operation performance and low energy consumption in the process of preparing ozone and is beneficial to the heat dissipation of electrode slices; and the prepared ozone can be taken away quickly, the dissolving amount of the ozone in water is improved, and the concentration of the ozone is further improved.
The purpose of the utility model is realized through the following technical scheme:
an electrolytic ozone generator comprises a cavity, an electrode plate and a diaphragm, wherein the electrode plate and the diaphragm are arranged in the cavity, the electrode plate comprises a positive plate and a negative plate, and the diaphragm is arranged between the positive plate and the negative plate; wherein, the two ends of the cavity are respectively provided with a water inlet and a water outlet; one side surface of the diaphragm is parallel and opposite to the positive plate, and the other side surface of the diaphragm is parallel and opposite to the negative plate; the diaphragm is a diaphragm without a through hole; annular flow guide channels are arranged between the peripheries of the positive plate, the negative plate and the diaphragm and the inner wall of the cavity; a water flow distribution space is arranged between the water inlet and the electrode plate at the water inlet end and is respectively communicated with the annular flow guide channel and the through holes on the electrode plate at the water inlet end; the positive plate and the negative plate are electrically connected through water flowing through the positive plate and the negative plate.
The electrolytic ozone generator has the working principle that:
when the water electrolysis device works, water enters the cavity from the water inlet and reaches the water flow distribution space and is divided into two paths, one path of water flows into a gap between the electrode plate positioned at the water inlet end and the membrane through the through hole of the electrode plate positioned at the water inlet end of the cavity for electrolysis, part of water flows around the membrane under the blocking of the membrane and enters the annular flow guide channel, and then part of water enters the gap between the electrode plate positioned at the water outlet end and the membrane for electrolysis, in the electrolysis process, the positive plate is electrolyzed to generate ozone, and the negative plate is electrolyzed to generate hydrogen; after the other path of water enters the water flow distribution space, the water flow is dispersed to the periphery and enters the annular flow guide channel under the blocking of the electrode plate positioned at the water inlet end; through adjusting the size relation of the cross section of the annular flow guide channel and the cross section of the through hole of the electrode plate positioned at the water inlet end, the water velocity of the annular flow guide channel can be larger than that between the electrode plate and the diaphragm, so that the annular flow guide channel generates a Venturi effect, low pressure is generated near a high-speed flowing water body in the annular flow guide channel, and pressure difference is generated between a gap between the electrode plate and the diaphragm and the annular flow guide channel. Meanwhile, the water body flowing at high speed in the annular flow guide channel is also favorable for accelerating the heat of the electrode plate and improving the heat dissipation effect.
The utility model discloses a preferred scheme, wherein, the terminal surface of positive plate is towards the water inlet, and the terminal surface of negative pole piece is towards the delivery port. Namely, the positive plate is arranged at the water inlet end, and the negative plate is arranged at the water outlet end. The water flow distribution device has the advantages that after the water body enters the water flow distribution space, a part of the water body enters the gap between the positive plate and the diaphragm from the through hole of the positive plate for electrolysis, a part of the water body enters the annular flow guide channel from the water flow distribution space, and the water body rapidly flows in the annular flow guide channel to form a negative pressure adsorption effect, so that the positive plate is taken away in time to generate ozone and ozone water; the anode plate is arranged at the water inlet end of the cavity, so that the flow velocity of the annular flow guide channel at the water inlet end is accelerated, the ozone adsorption capacity and speed of the annular flow guide channel are further improved, and the dissolving amount of ozone in water is increased; in addition, because the diaphragm is of a structure without through holes, all water entering the gap between the positive plate and the diaphragm flows away from the annular flow guide channel, so that ozone generated by electrolysis of the positive plate can be completely taken away, and the dissolving amount of the ozone in water is further improved. Meanwhile, a part of water body passes through the through holes of the electrode plates, a part of water body flows from the annular flow guide channel, the flow of the two water bodies plays a cooling role, and particularly, the water body which rapidly flows in the annular flow guide channel is more favorable for heat dissipation of the positive electrode plate, so that the stability of electrolysis is improved, and the electrolysis performance is improved.
The utility model discloses a preferred scheme, wherein, electrolysis formula ozone generator still includes the subassembly of intaking that is located the cavity intake end; the water inlet assembly comprises a water inlet pipe and an adjusting port which is arranged on the water inlet pipe and used for adjusting the water flow speed and pressure, one end of the water inlet pipe is connected with a water source, and the other end of the water inlet pipe is connected with the water inlet; and the water body which is divided out by the adjusting port flows back to the water source. By adopting the structure, when the power of the electrode plate is too high, the electrode plate can generate heat seriously, and the water flow speed of the water inlet pipe is increased by arranging the adjusting port for adjustment, so that the heat of the electrode plate is taken away, the cooling effect is realized, the power is also stabilized, and the service life of the electrode plate is prolonged; in addition, the flow velocity is accelerated, and the ozone adsorption capacity of the annular flow guide channel is improved.
Furthermore, the adjusting port is internally provided with a steel ball with a notch for adjusting water flow, and the water flow is adjusted by replacing the steel balls with the notches of different sizes.
The utility model discloses a preferred scheme, wherein, positive plate with the through-hole of negative pole piece is adjusted well each other and axial projection overlaps.
The utility model discloses a preferred scheme, wherein, positive plate with the through-hole of negative pole piece staggers each other and axial projection does not overlap.
Preferably, the number of the through holes of the positive plate and the negative plate is multiple. The method has the advantages of further improving the contact area between the water body and the surface of the positive plate or the negative plate and promoting the electrolysis efficiency.
Further, the area of the through holes of the positive plate or the negative plate accounts for 5% -80% of the total area of the positive plate or the negative plate. The benefit that sets up like this lies in, improves the heat radiating area of water and positive plate and negative pole piece, promotes the ozone electrolysis efficiency of positive plate on the one hand, prepares the higher ozone water of concentration, and on the other hand improves the radiating efficiency, improves current density 10% and does not burn the diaphragm, further improves the life of diaphragm.
The utility model discloses a preferred scheme, wherein, positive plate perhaps negative pole piece with be equipped with between the cavity inner wall and be used for positive plate or the negative pole piece carries out the displacement buffer zone that the displacement cushioned. When the water pressure is too large or too small, the displacement buffer area can enable the distance between the positive plate and the negative plate to be automatically adjusted according to the water pressure, so that the distance between the positive plate and the negative plate tends to be stable, and the action of the scouring force of the positive plate or the negative plate is increased.
Preferably, a buffer assembly for buffering the water pressure borne by the positive plate or the negative plate is arranged on the displacement buffer area.
Furthermore, the buffer assembly is an elastic piece, the elastic piece is axially arranged, one end of the elastic piece acts on the positive plate or the negative plate, and the other end of the elastic piece acts on the inner wall of the cavity. Through setting up the elastic component, can be according to the different water pressures in the cavity for positive plate or negative pole piece automatic adjustment and diaphragm between the clearance, make the cavity can adapt to the inflow of difference also can normally work and do not damage positive plate or negative pole piece, guaranteed positive plate and negative pole piece electrolysis process and tend to stably, when playing the reduction energy consumption, can also effectively protect positive plate or negative pole piece and improve life.
Preferably, the elastic member is any one of a spring, a tower spring or a spring plate.
Preferably, the membrane is a PEM membrane, and the PEM membrane has good proton conductivity and good electrochemical stability.
Preferably, the through hole of the positive electrode plate and/or the negative electrode plate is any one of a circle, a triangle, a rectangle, a trapezoid, a square, a parallelogram, a rhombus or an irregular shape.
Preferably, the negative electrode sheet is any one of stainless steel, a carbon material, various metal materials, a metal oxide, a non-metal conductive material and a composite material; the anode plate material is any one of diamond, platinum, titanium, electrolytic water electrode wear-resistant materials, or conductive ceramics, semiconductors, carbon materials, graphite materials and other metal materials.
Compared with the prior art, the utility model following beneficial effect has:
1. in the utility model, because the water flow distribution space is arranged, the water body flows in two paths after entering the cavity, one path of water body flows into the gap between the electrode plate and the membrane at the water inlet end through the through hole of the electrode plate at the water inlet end of the cavity for electrolysis, the other path flows from the annular flow guide channel, and the membrane is in a non-porous structure, so that the water body passing through the through hole is blocked, the water body flow velocity at the position is slower, the water body flow velocity at the annular flow guide channel is faster, the annular flow guide channel generates Venturi effect, low pressure is generated near the high-speed flowing water body, and pressure difference is generated between the gap between the electrode plate and the membrane of the cavity and the annular flow guide channel, therefore, the water flow in the annular flow guide channel generates adsorption effect on the water body in the gap between the electrode plate and the membrane, and ozone water generated by, can take away the ozone of preparation fast, improve ozone in aquatic dissolved quantity, and then improved ozone concentration.
2. The utility model discloses in, after the water got into rivers distribution space, some water passes from the through-hole of positive plate or negative pole piece, partly flows from annular water conservancy diversion passageway, positive plate and negative pole piece produce a large amount of heats in the electrolysis process, the flow of two way waters plays and adjusts positive plate or negative pole piece cooling effect, more importantly, the water in annular water conservancy diversion passageway flows fast, can take away the heat of positive plate or negative pole piece more fast, not only improve the stability of electrolysis, the life of positive plate and negative pole piece has still been improved.
3. The utility model discloses in, because be equipped with the through-hole on positive plate or the negative pole piece for the effective area of contact grow of water and electrode slice has improved electrolysis efficiency and can prepare the higher ozone water of concentration, also can improve the radiating efficiency of electrode slice simultaneously, and then improves the life of electrode slice.
4. The utility model discloses in, when the water gets into to lie in the clearance between the electrode slice and the diaphragm of intaking the end from the through-hole that passes through of intaking the end electrode slice, because the diaphragm is no through-hole diaphragm, the water scatters to all around under the effect of blockking of diaphragm, the diaphragm will receive the impact force backward movement of water, though the diaphragm and the clearance grow that lies in between the electrode slice of intaking the end, but because blockking of diaphragm, make the electrode slice that lies in the end of water outlet not receive axial impact force, make the fluctuation distance between positive plate and the negative pole piece reduce greatly, thereby reduce operating voltage, the effect that reduces the energy consumption has been played.
5. The utility model discloses in, rivers pass from positive plate or negative pole piece's through-hole after intaking the end entering water flow distribution space, and partly water flows from annular water conservancy diversion passageway to reduce the impact force to intaking the end electrode piece, make into water the end electrode piece range of floating reduce greatly, the stability of the voltage that improves, make the electrolysis operation performance more stable.
Drawings
Fig. 1-3 are schematic structural views of a first embodiment of an electrolytic ozone generator in the present invention, in which fig. 1 is a perspective view, fig. 2 is a right side view, and fig. 3 is a front view.
Fig. 4 is a vertical sectional view of an electrolytic ozone generator according to the present invention.
Fig. 5 is a schematic diagram of the internal structure of the cavity in the present invention.
Fig. 6-7 are schematic structural views of a third embodiment of an electrolytic ozone generator in the present invention, wherein fig. 6 is a perspective view of the electrolytic ozone generator without a water inlet assembly and a spring, and fig. 7 is a perspective view of the internal structure of the chamber.
Fig. 8 is a schematic structural diagram of a fourth embodiment of an electrolytic ozone generator according to the present invention.
Detailed Description
In order to make those skilled in the art understand the technical solution of the present invention well, the present invention will be further described below with reference to the following examples and drawings, but the embodiments of the present invention are not limited thereto.
Example 1
Referring to fig. 1-5, the electrolytic ozone generator in this embodiment includes a cavity 1, a positive plate 2 and a negative plate 3 disposed inside the cavity 1, a membrane 4 disposed between the positive plate 2 and the negative plate 3 for proton exchange, a water inlet assembly 5 disposed at one end of the cavity 1 close to the positive plate 2, and a spring 6 disposed at one end of the cavity 1 close to the negative plate 3; one end of the spring 6 acts on the negative plate 3, and the other end acts on the inner wall of the cavity 1; the water inlet end of the cavity 1 is provided with a water inlet, the water outlet end is provided with a water outlet, the water inlet is communicated with the water inlet assembly 5, the positive plate 2 is close to the water inlet, and the negative plate 3 is close to the water outlet. Through setting up spring 6, too big or when the water pressure is too little, can be according to the different water pressures in the cavity 1, make negative pole piece 3 automatic adjustment and the positive plate 2 between the effect of spring 6 distance, make the distance between the two tend to stably, make cavity 1 can adapt to different inflow also can normally work and do not damage negative pole piece 3, the stability of positive plate 2 with 3 electrolysis processes of negative pole piece has been guaranteed, when playing the reduction energy consumption, can also effectively protect negative pole piece 3, improve the life of negative pole piece 3 and positive plate 2.
Referring to fig. 1 to 5, the outline of each of the cavity 1, the positive plate 2, the negative plate 3 and the diaphragm 4 is rectangular, one side surface of the diaphragm 4 is parallel to and opposite to the positive plate 2, and the other side surface of the diaphragm 4 is parallel to and opposite to the negative plate 3; the positive plate 2 is provided with circular first through holes 2-1, the number of the first through holes 2-1 is 6, and the first through holes are uniformly arranged on the positive plate 2 in two rows; the negative plate 3 is provided with second through holes 3-1, the number of the second through holes 3-1 is 6, the second through holes are uniformly arranged on the negative plate 3 in two rows, and the first through holes 2-1 and the second through holes 3-1 are aligned with each other and are overlapped in axial projection; the diaphragm 4 is a diaphragm 4 without a through hole. By adopting the structure, the surface contact area of the water body and the positive plate 2 and the negative plate 3 can be effectively promoted by arranging the through holes, the electrolysis efficiency can be promoted, and the ozone water with higher concentration can be prepared, so that the electrolysis product is discharged in the circumferential direction as soon as possible without generating an inhibiting effect, the heat dissipation efficiency is improved, and the energy consumption is reduced. Adopt 4 structures of sclausura diaphragm, when the water enters into the clearance between positive plate 2 and the diaphragm 4 from the through-hole of passing through of positive plate 2, because diaphragm 4 is no through-hole diaphragm 4, the water scatters around to under the effect of blockking of diaphragm 4, diaphragm 4 will receive the impact force backward movement of water, although the clearance grow between diaphragm 4 and the positive plate 2, but because blockking of diaphragm 4, make negative pole piece 3 not receive axial impact force, make the distance between positive plate 2 and the negative pole piece 3 tend to stably, thereby the stability of voltage has been guaranteed, further the effect of reducing the energy consumption has been played.
Referring to fig. 1-5, peripheral annular gaps exist between the peripheries of the positive plate 2, the negative plate 3 and the diaphragm 4 and the inner wall of the cavity 1, and the peripheral annular gaps form an annular flow guide channel 7; the ratio of the area of the first through hole 2-1 to the area of the annular flow guide channel 7 is 0.1-1; a water flow distribution space 8 is arranged between the water inlet and the positive plate 2, and the water flow distribution space 8 is communicated with the annular flow guide channel 7; the positive plate 2 is connected with the positive pole of a power supply, the negative plate 3 is connected with the negative pole of the power supply, and the positive plate 2 is electrically connected with the negative plate 3 through a water body (electrolytic solution). And the power supply of the positive plate 2 and the negative plate 3 is switched on, so that the water body in the cavity 1 is electrolyzed, the positive plate 2 is electrolyzed to generate ozone, and the negative plate 3 is electrolyzed to generate hydrogen. Because the water flow distribution space 8 is arranged, water flows in two paths after entering the cavity 1, one path of water flows into a gap between the positive plate 2 and the membrane 4 through the first through hole 2-1 of the positive plate 2 positioned at the water inlet end of the cavity 1 for electrolysis, the other path of water flows from the annular flow guide channel 7, and the membrane 4 is of a non-porous structure, so that the water passing through the first through hole 2-1 is blocked, the water flow velocity at the position is slow, the water flow velocity in the annular flow guide channel 7 is increased, the annular flow guide channel 7 generates a Venturi effect, low pressure is generated near the high-speed flowing water, and pressure difference is generated between the middle part of the cavity 1 and the annular flow guide channel 7, therefore, water flow in the annular flow guide channel 7 generates adsorption, and gas generated by electrolysis on the positive plate 2 or the negative plate 3 and ozone water are adsorbed into the annular flow guide channel 7, can take away the ozone of preparation fast, improve ozone in aquatic dissolved quantity, and then improved ozone concentration.
Referring to fig. 1-5, a space between the negative electrode plate 3 and the inner wall of the cavity 1 forms a displacement buffer area 9 for performing displacement buffering on the negative electrode plate 3, the spring 6 is disposed on the displacement buffer area 9, and when the water pressure is too large or too small, the displacement buffer area 9 can automatically adjust the distance between the positive electrode plate 2 and the negative electrode plate 3 according to the water pressure, so that the distance between the positive electrode plate 2 and the negative electrode plate 3 tends to be stable, and the scouring force effect of the positive electrode plate 2 or the negative electrode plate 3 is increased.
Referring to fig. 1-5, the water inlet assembly 5 comprises a water inlet pipe 5-1 and an adjusting port 5-2 arranged on the water inlet pipe 5-1 for adjusting the speed and pressure of water flow, wherein one end of the water inlet pipe 5-1 is connected with a water source, and the other end is connected with the water inlet; the water body branched out by the adjusting port 5-2 flows back to the water source; the adjusting port 5-2 is internally provided with a steel ball with a notch for adjusting water flow, and the water flow is adjusted by replacing the steel balls with notches of different sizes. By adopting the structure, when the power of the positive plate 2 is too large, the positive plate 2 generates heat seriously, and the water flow speed of the water inlet pipe 5-1 is increased by arranging the adjusting port 5-2 for adjustment, so that the heat of the positive plate 2 is taken away, the cooling effect is achieved, the power is also stabilized, and the service life of the electrode plate is prolonged; in addition, the flow velocity is accelerated, and the capability of the annular flow guide channel 7 for adsorbing ozone is also improved.
Referring to fig. 1 to 5, the area of the first through hole 2-1 of the positive plate 2 accounts for 5 to 80 percent of the total area of the positive plate 2; the area of the second through hole 3-1 of the negative plate 3 accounts for 5-80% of the total area of the negative plate 3. The benefit that sets up like this lies in, improves the heat radiating area of water and positive plate 2 and negative pole piece 3, promotes the ozone electrolysis efficiency of positive plate 2 on the one hand, prepares the higher ozone water of concentration, and on the other hand improves the radiating efficiency, improves current density 10% and does not burn diaphragm 4, further improves diaphragm 4's life.
Referring to fig. 1 to 5, the buffer assembly is an elastic member, and the elastic member is axially disposed, and one end of the elastic member acts on the positive plate 2 or the negative plate 3, and the other end of the elastic member acts on the inner wall of the cavity 1. Through setting up the elastic component, can be according to the different water pressures in the cavity 1 for positive plate 2 or 3 automatic adjustment of negative pole piece and diaphragm 4 between the clearance, make cavity 1 can adapt to the different inflow and also can normally work and do not damage positive plate 2 or negative pole piece 3, guaranteed positive plate 2 and 3 electrolysis processes of negative pole piece and tend to stably, when playing the reduction energy consumption, can also effectively protect positive plate 2 or negative pole piece 3 and improve life.
Referring to fig. 1-5, the positive plate 2 is made of diamond, the negative plate 3 is made of stainless steel, the membrane 4 is a PEM membrane, and the PEM membrane has good proton conductivity and electrochemical stability.
Referring to fig. 1-5, the electrolytic ozone generator operates according to the following principle:
when the water electrolysis device works, water is conveyed through the water inlet pipe 5-1, enters the cavity 1 from the water inlet and reaches the water flow distribution space 8 and is divided into two paths, one path of water flows into a gap between the positive plate 2 and the diaphragm 4 at the water inlet end through the through hole of the positive plate 2 at the water inlet end of the cavity 1 for electrolysis, part of water flows around the diaphragm 4 under the blocking of the diaphragm 4 and enters the annular flow guide channel 7, then part of water enters the space between the negative plate 3 at the water outlet end and the diaphragm 4 for electrolysis, ozone is generated by the electrolysis of the positive plate 2, and hydrogen is generated by the electrolysis of the negative plate 3 in the electrolysis process; the membrane 4 is of a non-porous structure, so that water passing through the through hole of the positive plate 2 at the water inlet end is blocked, and the flow rate of the water at the position is low; after the other path of water enters the water flow distribution space 8, the water flow is dispersed to the periphery under the blocking of the positive plate 2 or the negative plate 3 at the water inlet end and enters the annular flow guide channel 7. By adjusting the size relationship between the cross section of the annular flow guide channel 7 and the cross section of the through hole of the electrode plate at the water inlet end, the water flow speed of the annular flow guide channel 7 can be made to be larger than the water flow speed between the electrode plate and the membrane 4, so that the annular flow guide channel 7 generates a Venturi effect, low pressure is generated near a high-speed flowing water body in the annular flow guide channel 7, and pressure difference is generated between the gap between the electrode plate and the membrane 4 and the annular flow guide channel 7, therefore, the water flow in the annular flow guide channel 7 generates adsorption, ozone and ozone water generated by electrolysis on the positive plate 2 are adsorbed into the annular flow guide channel 7, the prepared ozone can be taken away quickly, the dissolving amount of the ozone in water is improved, and then the ozone concentration is improved, and finally, the ozone and ozone water are discharged from a water outlet of the cavity through the conveying of the annular flow guide channel 7, so that the preparation of the ozone is completed. Meanwhile, the water flowing at high speed in the annular flow guide channel 7 is also beneficial to accelerating the heat of the electrode plate and improving the heat dissipation effect.
The flow velocity of the annular flow guide channel 7 can be adjusted through the adjusting port 5-2, and when the power of the positive plate 2 and the negative plate 3 is too high and the heat is serious, the heat dissipation of the positive plate 2 and the negative plate is facilitated by increasing the flow velocity of the annular flow guide channel 7; because positive plate 2 is close to the water inlet, the velocity of flow of the end of intaking of annular water conservancy diversion passageway 7 is more accelerated to further improve the ability of annular water conservancy diversion passageway 7 absorption ozone, improve the dissolved volume of ozone in aqueous.
Referring to the following table, the technical solutions in the present embodiment are tested and compared with two other technical solutions, and the materials used for comparing the two technical solutions are the same for the positive electrode sheet 2, the membrane sheet 4 and the negative electrode sheet 3, where table 1 is a test comparison between the present embodiment and the first technical solution (patent publication No. CN107177861B), and the test conditions are as follows: the area of the electrode plate of the first technical scheme is 2 times that of the electrode plate of the first technical scheme, water flow and water temperature are unchanged, and power consumption and concentration of water conductivity test are changed. Table 2 shows the comparison between the present example and the second technical solution (patent application publication No. CN109487293A), the test conditions are as follows: the area of the electrode plate of the second technical scheme is the same as that of the electrode plate of the embodiment, the current density is the same, the water flow and the water temperature are unchanged, and the power consumption and the concentration of the water conductivity test are changed.
TABLE 1
TABLE 2
As can be seen from the test data, the test results in Table 1 are: compared with the first technical scheme, in the same water environment, the technical scheme of the embodiment reduces the area of the electrode plate by 50%, and under the same current, the ozone concentration in the water is improved by 1 time.
The test results in table 2 are: compared with the second technical scheme, in the same water environment, the energy consumption is reduced by 40% in the embodiment, and the ozone concentration in the water is improved by 20% under the same current density.
Example 2
The other structures in this embodiment are the same as embodiment 1, except that: the first through hole 2-1 of the positive plate 2 and the second through hole 3-1 of the negative plate 3 are staggered with each other, and the axial projections are not overlapped. By adopting the structure, the surface contact area between the water body and the positive plate 2 or the negative plate 3 can be effectively promoted, the electrolytic efficiency can be promoted, the ozone water with higher concentration can be prepared, the electrolytic product can be discharged circumferentially as soon as possible without generating an inhibiting effect, the heat dissipation efficiency is improved, and the energy consumption is reduced.
Example 3
Referring to fig. 6 to 7, the other structure in the present embodiment is the same as embodiment 1 except that: the outline of the cavity 1, the outline of the positive plate 2, the outline of the negative plate 3 and the outline of the diaphragm 4 are all circular, one side surface of the diaphragm 4 is parallel and opposite to the positive plate 2, and the other side surface of the diaphragm 4 is parallel and opposite to the negative plate 3; the positive plate 2 is provided with circular first through holes 2-1, the number of the first through holes 2-1 is 6, one of the first through holes is arranged at the circle center of the positive plate 2, and the other 5 through holes are arranged in a circle array around the circle center of the positive plate 2; the cathode plate 3 is provided with second through holes 3-1, the number of the second through holes 3-1 is 6, one of the second through holes is arranged at the circle center of the anode plate 2, the other 5 second through holes are arranged around the circle center of the anode plate 2 in a circumferential array, the first through holes 2-1 and the second through holes 3-1 are aligned with each other, and the axial projections of the first through holes and the second through holes are overlapped. By adopting the structure, the circular cavity 1 is arranged, so that the water body can flow in the circular flow guide channel 7 in the cavity 1, and the speed of preparing ozone is improved; through setting up a plurality of through-holes, can effectively promote the surface contact area of water and positive plate 2 and negative pole piece 3, not only can promote electrolysis efficiency and can prepare the higher ozone water of concentration, make the electrolysis result discharge as early as possible circumference and can not produce the inhibitory action, improve the radiating efficiency, reduce the energy consumption.
Example 4
Referring to fig. 8, the other structure in the present embodiment is the same as embodiment 1 except that: the water inlet assembly 5 is arranged at one end, close to the negative plate 3, of the cavity 1, the spring 6 is arranged at one end, close to the positive plate 2, of the cavity 1, and a water flow distribution space 8 is formed between the negative plate 3 and the water inlet. Namely, the negative plate 3 is arranged at the water inlet end of the cavity 1, and the positive plate 2 is arranged at the water outlet end of the cavity 1. Adopt above-mentioned structure, negative pole piece 3 is close to the water inlet, and the velocity of flow of annular water conservancy diversion passageway 7 intake the end is more accelerated to be favorable to taking away negative pole piece 3 and producing hydrogen, also play better radiating effect to negative pole piece 3 simultaneously, make the scaling problem in negative pole piece 3 obtain solving, along with the reduction of scaling, voltage tends towards stability, is favorable to prolonging the life of negative pole piece 3.
Example 5
The other structures in this embodiment are the same as embodiment 1, except that: the first through hole 2-1 of the positive plate 2 and the second through hole 3-1 of the negative plate 3 may be any one of a triangle, a rectangle, a trapezoid, a square, a parallelogram, a rhombus and an irregular shape.
Example 6
The other structures in this embodiment are the same as embodiment 1, except that: the buffer assembly is a magnetic device, a magnetic field generated by the magnetic device acts on the electrode plate to generate axial acting force on the electrode plate, and the axial acting force is used for balancing water flow impact force borne by the electrode plate, so that the electrode plate is in a balanced state, for example, when the cathode plate needs to be set to be in a movable state, magnets with the same polarity are arranged on the inner wall of the cavity and the cathode plate, and the functions can be realized.
The above is the preferred embodiment of the present invention, but the embodiment of the present invention is not limited by the above, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be equivalent replacement modes, and all are included in the scope of the present invention.
Claims (15)
1. An electrolytic ozone generator comprises a cavity, an electrode plate and a diaphragm, wherein the electrode plate and the diaphragm are arranged in the cavity, the electrode plate comprises a positive plate and a negative plate, and the diaphragm is arranged between the positive plate and the negative plate; wherein, the two ends of the cavity are respectively provided with a water inlet and a water outlet; one side surface of the diaphragm is parallel and opposite to the positive plate, and the other side surface of the diaphragm is parallel and opposite to the negative plate; the diaphragm is a diaphragm without a through hole; annular flow guide channels are arranged between the peripheries of the positive plate, the negative plate and the diaphragm and the inner wall of the cavity; a water flow distribution space is arranged between the water inlet and the electrode plate at the water inlet end and is respectively communicated with the annular flow guide channel and the through holes on the electrode plate at the water inlet end; the positive plate and the negative plate are electrically connected through water flowing through the positive plate and the negative plate.
2. The electrolytic ozone generator of claim 1, wherein the end face of the positive plate faces the water inlet and the end face of the negative plate faces the water outlet.
3. The electrolytic ozone generator of claim 1 or claim 2 further comprising a water inlet assembly located at the water inlet end of the chamber; the water inlet assembly comprises a water inlet pipe and an adjusting port which is arranged on the water inlet pipe and used for adjusting the water flow speed and pressure, one end of the water inlet pipe is connected with a water source, and the other end of the water inlet pipe is connected with the water inlet; and the water body which is divided out by the adjusting port flows back to the water source.
4. The electrolytic ozone generator of claim 3, wherein the adjusting port is internally provided with a steel ball with a notch for adjusting water flow, and the adjustment of water flow is realized by replacing the steel balls with notches of different sizes.
5. The electrolytic ozone generator of any one of claims 1, 2 or 4, wherein the through holes of the positive plate and the negative plate are aligned and overlap in axial projection.
6. The electrolytic ozone generator of any one of claims 1, 2 or 4, wherein the through holes of the positive plate and the negative plate are staggered and do not overlap in axial projection.
7. The electrolytic ozone generator of any one of claims 1, 2 or 4, wherein the number of the through holes of the positive plate and the negative plate is plural.
8. The electrolytic ozone generator of any one of claims 1, 2 or 4, wherein the area of the through holes of the positive or negative plate accounts for 5-80% of the total area of the positive or negative plate.
9. The electrolytic ozone generator of any one of claims 1, 2 or 4, wherein a displacement buffer area for buffering displacement of the positive plate or the negative plate is arranged between the positive plate or the negative plate and the inner wall of the cavity.
10. The electrolytic ozone generator of claim 9, wherein the displacement buffer zone is provided with a buffer component for buffering water pressure applied to the positive plate or the negative plate.
11. The electrolytic ozone generator of claim 10, wherein the buffer assembly is an elastic member axially disposed with one end acting on the positive plate or the negative plate and the other end acting on the inner wall of the chamber.
12. The electrolytic ozone generator of claim 11, wherein the elastic member is any one of a spring, a tower spring or a leaf spring.
13. An electrolytic ozone generator according to any of claims 1, 2 or 4 characterised in that the membrane is a PEM membrane.
14. The electrolytic ozone generator of claim 1, wherein the through holes of the positive plate and/or the negative plate are any one of circular, triangular, rectangular, trapezoidal, square, parallelogram, rhombus or irregular.
15. The electrolytic ozone generator of any one of claims 1, 2 or 4, wherein the negative plate is any one of stainless steel, carbon material, metal oxide, non-metal conductive material and composite material; the anode plate material is any one of diamond, platinum, titanium, an electrolytic water electrode wear-resistant material, conductive ceramics, a semiconductor, a carbon material and a graphite material.
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| CN202020618526.7U CN212247223U (en) | 2020-04-22 | 2020-04-22 | Electrolytic ozone generator |
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| CN202020618526.7U CN212247223U (en) | 2020-04-22 | 2020-04-22 | Electrolytic ozone generator |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111304678A (en) * | 2020-04-22 | 2020-06-19 | 广州市德百顺电气科技有限公司 | Electrolytic ozone generator |
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2020
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111304678A (en) * | 2020-04-22 | 2020-06-19 | 广州市德百顺电气科技有限公司 | Electrolytic ozone generator |
| CN111304678B (en) * | 2020-04-22 | 2024-11-01 | 广州德百顺蓝钻科技有限公司 | Electrolytic ozone generator |
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